HUP0300468A2 - Method and apparatus for separating particles from hot gases - Google Patents
Method and apparatus for separating particles from hot gasesInfo
- Publication number
- HUP0300468A2 HUP0300468A2 HU0300468A HUP0300468A HUP0300468A2 HU P0300468 A2 HUP0300468 A2 HU P0300468A2 HU 0300468 A HU0300468 A HU 0300468A HU P0300468 A HUP0300468 A HU P0300468A HU P0300468 A2 HUP0300468 A2 HU P0300468A2
- Authority
- HU
- Hungary
- Prior art keywords
- gas
- walls
- gas space
- reaction chamber
- vortex
- Prior art date
Links
- 239000002245 particle Substances 0.000 title abstract 3
- 238000000034 method Methods 0.000 title abstract 2
- 239000007789 gas Substances 0.000 title 1
- 239000007787 solid Substances 0.000 abstract 2
- 238000007599 discharging Methods 0.000 abstract 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract 1
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
- B01J8/24—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique
- B01J8/26—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with two or more fluidised beds, e.g. reactor and regeneration installations
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D45/00—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
- B01D45/12—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by centrifugal forces
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/0053—Details of the reactor
- B01J19/006—Baffles
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/005—Separating solid material from the gas/liquid stream
- B01J8/0055—Separating solid material from the gas/liquid stream using cyclones
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
- B01J8/24—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique
- B01J8/38—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with fluidised bed containing a rotatable device or being subject to rotation or to a circulatory movement, i.e. leaving a vessel and subsequently re-entering it
- B01J8/384—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with fluidised bed containing a rotatable device or being subject to rotation or to a circulatory movement, i.e. leaving a vessel and subsequently re-entering it being subject to a circulatory movement only
- B01J8/388—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with fluidised bed containing a rotatable device or being subject to rotation or to a circulatory movement, i.e. leaving a vessel and subsequently re-entering it being subject to a circulatory movement only externally, i.e. the particles leaving the vessel and subsequently re-entering it
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
- B04C5/00—Apparatus in which the axial direction of the vortex is reversed
- B04C5/08—Vortex chamber constructions
- B04C5/081—Shapes or dimensions
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
- B04C5/00—Apparatus in which the axial direction of the vortex is reversed
- B04C5/08—Vortex chamber constructions
- B04C5/085—Vortex chamber constructions with wear-resisting arrangements
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
- B04C5/00—Apparatus in which the axial direction of the vortex is reversed
- B04C5/20—Apparatus in which the axial direction of the vortex is reversed with heating or cooling, e.g. quenching, means
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
- B04C5/00—Apparatus in which the axial direction of the vortex is reversed
- B04C5/24—Multiple arrangement thereof
- B04C5/28—Multiple arrangement thereof for parallel flow
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23C—METHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN A CARRIER GAS OR AIR
- F23C10/00—Fluidised bed combustion apparatus
- F23C10/02—Fluidised bed combustion apparatus with means specially adapted for achieving or promoting a circulating movement of particles within the bed or for a recirculation of particles entrained from the bed
- F23C10/04—Fluidised bed combustion apparatus with means specially adapted for achieving or promoting a circulating movement of particles within the bed or for a recirculation of particles entrained from the bed the particles being circulated to a section, e.g. a heat-exchange section or a return duct, at least partially shielded from the combustion zone, before being reintroduced into the combustion zone
- F23C10/08—Fluidised bed combustion apparatus with means specially adapted for achieving or promoting a circulating movement of particles within the bed or for a recirculation of particles entrained from the bed the particles being circulated to a section, e.g. a heat-exchange section or a return duct, at least partially shielded from the combustion zone, before being reintroduced into the combustion zone characterised by the arrangement of separation apparatus, e.g. cyclones, for separating particles from the flue gases
- F23C10/10—Fluidised bed combustion apparatus with means specially adapted for achieving or promoting a circulating movement of particles within the bed or for a recirculation of particles entrained from the bed the particles being circulated to a section, e.g. a heat-exchange section or a return duct, at least partially shielded from the combustion zone, before being reintroduced into the combustion zone characterised by the arrangement of separation apparatus, e.g. cyclones, for separating particles from the flue gases the separation apparatus being located outside the combustion chamber
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J15/00—Arrangements of devices for treating smoke or fumes
- F23J15/02—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material
- F23J15/022—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material for removing solid particulate material from the gasflow
- F23J15/027—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material for removing solid particulate material from the gasflow using cyclone separators
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00761—Details of the reactor
- B01J2219/00763—Baffles
- B01J2219/00765—Baffles attached to the reactor wall
- B01J2219/0077—Baffles attached to the reactor wall inclined
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/02—Apparatus characterised by their chemically-resistant properties
- B01J2219/0204—Apparatus characterised by their chemically-resistant properties comprising coatings on the surfaces in direct contact with the reactive components
- B01J2219/0218—Apparatus characterised by their chemically-resistant properties comprising coatings on the surfaces in direct contact with the reactive components of ceramic
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J2900/00—Special arrangements for conducting or purifying combustion fumes; Treatment of fumes or ashes
- F23J2900/15025—Cyclone walls forming heat exchangers
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J2900/00—Special arrangements for conducting or purifying combustion fumes; Treatment of fumes or ashes
- F23J2900/15026—Cyclone separators with horizontal axis
Abstract
Eljárás és berendezés szilárd részecskék szeparálására fluidágyasreaktor reakciókamrájából (20) kiáramló gáztól olyan centrifugálisszeparátor elrendezésben, amely tartalmaz egy horizontális iránybanvertikális irányú planáris vízcső panelekből álló falak általdefiniált örvénykamrát (70, 70', 70<), amely falak belseje legalábbrészben hőálló burkolattal ellátott, és amely falak az örvénykamrábanolyan gázteret definiálnak, amely gáztérben legalább egy vertikálisgázörvény (84, 84') létrejön, továbbá tartalmaz legalább egy, a gázszámára a reakciókamrából a gáztérbe történő bevezetésére alkalmasbemeneti csövet (82, 82'), legalább egy, a megtisztított gáz gáztérbőltörténő elvezetésére alkalmas kimeneti csövet, és legalább egy, aszeparált szilárd részecskéknek a gáztérből történő kivezetésérealkalmas visszavezető csövet. A találmány lényege, hogy aszeparátorösszeállítás biztosítja, hogy a reakciókamrából kiáramló gázaz örvénykamrában legalább egy, a külső falak belső oldalán hőállóburkolattal lekerekített, és a sarkot alkotó vertikális irányú külsőfalak által bezárt legalább 108 fokos szöggel rendelkező sarokkalütközzön. ÓMethod and device for separating solid particles from the gas flowing out of the reaction chamber (20) of a fluidized bed reactor in a centrifugal separator arrangement that includes a vortex chamber defined by walls (70, 70', 70<) consisting of horizontal and vertical planar water pipe panels, the inside of which walls are at least partially covered with a heat-resistant cover, and which walls in the vortex chamber define a gas space in which at least one vertical gas vortex (84, 84') is created, and also contains at least one inlet pipe (82, 82') suitable for introducing the gas from the reaction chamber into the gas space, at least one suitable for removing the purified gas from the gas space outlet pipe and at least one return pipe suitable for discharging separated solid particles from the gas space. The essence of the invention is that the separator assembly ensures that the gas flowing out of the reaction chamber collides with at least one corner in the vortex chamber, which is rounded on the inner side of the outer walls with a heat-resistant cover and enclosed by the vertical outer walls forming the corner, with an angle of at least 108 degrees. HE
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FI20000832A FI114289B (en) | 2000-04-07 | 2000-04-07 | Device for separating particles from hot gases |
PCT/FI2001/000337 WO2001076722A1 (en) | 2000-04-07 | 2001-04-06 | Method and apparatus for separating particles from hot gases |
Publications (2)
Publication Number | Publication Date |
---|---|
HUP0300468A2 true HUP0300468A2 (en) | 2003-06-28 |
HU229183B1 HU229183B1 (en) | 2013-09-30 |
Family
ID=8558151
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
HU0300468A HU229183B1 (en) | 2000-04-07 | 2001-04-06 | Method and apparatus for separating particles from hot gases |
Country Status (18)
Country | Link |
---|---|
US (1) | US6802890B2 (en) |
EP (2) | EP1268036B1 (en) |
JP (1) | JP4284022B2 (en) |
KR (1) | KR100500303B1 (en) |
CN (1) | CN1434740A (en) |
AT (2) | ATE352361T1 (en) |
AU (1) | AU2001252308A1 (en) |
CA (1) | CA2404800C (en) |
CZ (1) | CZ300881B6 (en) |
DE (2) | DE60126363T2 (en) |
DK (1) | DK1268036T3 (en) |
ES (1) | ES2280361T3 (en) |
FI (1) | FI114289B (en) |
HU (1) | HU229183B1 (en) |
PL (1) | PL200528B1 (en) |
PT (1) | PT1268036E (en) |
RU (1) | RU2229345C1 (en) |
WO (1) | WO2001076722A1 (en) |
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US8981250B2 (en) | 2001-07-16 | 2015-03-17 | Foret Plasma Labs, Llc | Apparatus for treating a substance with wave energy from plasma and an electrical Arc |
US9481584B2 (en) | 2001-07-16 | 2016-11-01 | Foret Plasma Labs, Llc | System, method and apparatus for treating liquids with wave energy from plasma |
US8764978B2 (en) | 2001-07-16 | 2014-07-01 | Foret Plasma Labs, Llc | System for treating a substance with wave energy from an electrical arc and a second source |
US10188119B2 (en) | 2001-07-16 | 2019-01-29 | Foret Plasma Labs, Llc | Method for treating a substance with wave energy from plasma and an electrical arc |
US7622693B2 (en) | 2001-07-16 | 2009-11-24 | Foret Plasma Labs, Llc | Plasma whirl reactor apparatus and methods of use |
US7857972B2 (en) | 2003-09-05 | 2010-12-28 | Foret Plasma Labs, Llc | Apparatus for treating liquids with wave energy from an electrical arc |
EP1308213A1 (en) * | 2001-10-30 | 2003-05-07 | Alstom (Switzerland) Ltd | A centrifugal separator, in particular for a fluidized bed reactor device |
US7553348B2 (en) * | 2005-05-16 | 2009-06-30 | Aerosynthesis Llc | Inducing air |
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US8241405B2 (en) * | 2006-10-20 | 2012-08-14 | The University Of Kentucky Research Foundation | Fluid scrubber and spray booth including the fluid scrubber |
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US10267106B2 (en) | 2007-10-16 | 2019-04-23 | Foret Plasma Labs, Llc | System, method and apparatus for treating mining byproducts |
US9761413B2 (en) | 2007-10-16 | 2017-09-12 | Foret Plasma Labs, Llc | High temperature electrolysis glow discharge device |
US9516736B2 (en) | 2007-10-16 | 2016-12-06 | Foret Plasma Labs, Llc | System, method and apparatus for recovering mining fluids from mining byproducts |
US9185787B2 (en) | 2007-10-16 | 2015-11-10 | Foret Plasma Labs, Llc | High temperature electrolysis glow discharge device |
US11806686B2 (en) | 2007-10-16 | 2023-11-07 | Foret Plasma Labs, Llc | System, method and apparatus for creating an electrical glow discharge |
US9051820B2 (en) | 2007-10-16 | 2015-06-09 | Foret Plasma Labs, Llc | System, method and apparatus for creating an electrical glow discharge |
US9560731B2 (en) | 2007-10-16 | 2017-01-31 | Foret Plasma Labs, Llc | System, method and apparatus for an inductively coupled plasma Arc Whirl filter press |
US8278810B2 (en) | 2007-10-16 | 2012-10-02 | Foret Plasma Labs, Llc | Solid oxide high temperature electrolysis glow discharge cell |
US9230777B2 (en) | 2007-10-16 | 2016-01-05 | Foret Plasma Labs, Llc | Water/wastewater recycle and reuse with plasma, activated carbon and energy system |
US9445488B2 (en) | 2007-10-16 | 2016-09-13 | Foret Plasma Labs, Llc | Plasma whirl reactor apparatus and methods of use |
US8810122B2 (en) | 2007-10-16 | 2014-08-19 | Foret Plasma Labs, Llc | Plasma arc torch having multiple operating modes |
FR2925369B1 (en) * | 2007-12-21 | 2011-11-11 | Total France | METHOD FOR ANTI-EROSION COATING OF A WALL, ANTI-EROSION COATING AND USE THEREOF |
US10244614B2 (en) | 2008-02-12 | 2019-03-26 | Foret Plasma Labs, Llc | System, method and apparatus for plasma arc welding ceramics and sapphire |
CA2715973C (en) | 2008-02-12 | 2014-02-11 | Foret Plasma Labs, Llc | System, method and apparatus for lean combustion with plasma from an electrical arc |
US8904749B2 (en) | 2008-02-12 | 2014-12-09 | Foret Plasma Labs, Llc | Inductively coupled plasma arc device |
GB2481429A (en) * | 2010-06-24 | 2011-12-28 | Dickinson Legg Ltd | Flow division apparatus |
CN102226518B (en) * | 2011-02-01 | 2013-03-06 | 中国科学院工程热物理研究所 | Large-scale circulating fluidized bed boiler |
CN105143413B (en) | 2012-12-11 | 2017-07-04 | 弗雷特等离子实验室公司 | High-temperature reflux vortex reactor system, method and apparatus |
WO2014165255A1 (en) | 2013-03-12 | 2014-10-09 | Foret Plasma Labs, Llc | Apparatus and method for sintering proppants |
EP2884170A1 (en) | 2013-12-16 | 2015-06-17 | Doosan Lentjes GmbH | Fluidized bed apparatus |
EP2884169B1 (en) | 2013-12-16 | 2016-07-27 | Doosan Lentjes GmbH | Fluidized bed apparatus |
EP2884172A1 (en) | 2013-12-16 | 2015-06-17 | Doosan Lentjes GmbH | Fluidized bed syphon |
EP2884162A1 (en) | 2013-12-16 | 2015-06-17 | Doosan Lentjes GmbH | Fluidized bed heat exchanger |
EP2884163B1 (en) | 2013-12-16 | 2017-04-05 | Doosan Lentjes GmbH | Fluidized bed apparatus with a fluidized bed heat exchanger |
EP2884164A1 (en) | 2013-12-16 | 2015-06-17 | Doosan Lentjes GmbH | Fluidized bed heat exchanger |
EP2884165A1 (en) | 2013-12-16 | 2015-06-17 | Doosan Lentjes GmbH | Fluidized bed heat exchanger |
EP2884168A1 (en) | 2013-12-16 | 2015-06-17 | Doosan Lentjes GmbH | Fluidized bed apparatus and mounting components |
EP2884166A1 (en) | 2013-12-16 | 2015-06-17 | Doosan Lentjes GmbH | Fluidized bed heat exchanger |
EP2884167A1 (en) | 2013-12-16 | 2015-06-17 | Doosan Lentjes GmbH | Fluidized bed apparatus |
FI126040B (en) * | 2014-07-09 | 2016-06-15 | Amec Foster Wheeler En Oy | Particle separator and fluidized bed reactor that can be connected to a fluidized bed reactor |
EP3000525A1 (en) | 2014-09-26 | 2016-03-30 | Doosan Lentjes GmbH | Fluidized bed reactor |
PL3054215T3 (en) | 2015-02-04 | 2017-08-31 | Doosan Lentjes Gmbh | Fluidized bed heat exchanger |
EP3130849B1 (en) | 2015-08-11 | 2018-07-04 | Doosan Lentjes GmbH | Circulating fluidized bed furnace |
GB2546544B (en) * | 2016-01-22 | 2018-04-18 | Dyson Technology Ltd | Cyclonic separation apparatus |
PL3311073T3 (en) | 2016-09-07 | 2020-11-16 | Doosan Lentjes Gmbh | Circulating fluidized bed apparatus |
RU2675644C1 (en) * | 2017-10-18 | 2018-12-21 | Евгений Михайлович Пузырёв | Boiler with circulating layer |
CN112384294A (en) * | 2018-07-02 | 2021-02-19 | 奥图泰(芬兰)公司 | Apparatus and method for cooling fine particle solids |
JP7467888B2 (en) | 2019-11-05 | 2024-04-16 | 株式会社Ihi | Fluidized Bed Systems |
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-
2000
- 2000-04-07 FI FI20000832A patent/FI114289B/en not_active IP Right Cessation
-
2001
- 2001-04-06 AT AT04014624T patent/ATE352361T1/en not_active IP Right Cessation
- 2001-04-06 PT PT01925608T patent/PT1268036E/en unknown
- 2001-04-06 JP JP2001574232A patent/JP4284022B2/en not_active Expired - Lifetime
- 2001-04-06 CA CA002404800A patent/CA2404800C/en not_active Expired - Fee Related
- 2001-04-06 DE DE60126363T patent/DE60126363T2/en not_active Expired - Lifetime
- 2001-04-06 CN CN01810814A patent/CN1434740A/en active Pending
- 2001-04-06 AT AT01925608T patent/ATE350129T1/en active
- 2001-04-06 US US10/240,773 patent/US6802890B2/en not_active Expired - Fee Related
- 2001-04-06 DK DK01925608T patent/DK1268036T3/en active
- 2001-04-06 WO PCT/FI2001/000337 patent/WO2001076722A1/en active IP Right Grant
- 2001-04-06 KR KR10-2002-7013439A patent/KR100500303B1/en active IP Right Grant
- 2001-04-06 EP EP01925608A patent/EP1268036B1/en not_active Expired - Lifetime
- 2001-04-06 ES ES01925608T patent/ES2280361T3/en not_active Expired - Lifetime
- 2001-04-06 DE DE60125737T patent/DE60125737T2/en not_active Expired - Lifetime
- 2001-04-06 PL PL357714A patent/PL200528B1/en unknown
- 2001-04-06 RU RU2002129505/15A patent/RU2229345C1/en not_active IP Right Cessation
- 2001-04-06 AU AU2001252308A patent/AU2001252308A1/en not_active Abandoned
- 2001-04-06 HU HU0300468A patent/HU229183B1/en not_active IP Right Cessation
- 2001-04-06 CZ CZ20023300A patent/CZ300881B6/en not_active IP Right Cessation
- 2001-04-06 EP EP04014624A patent/EP1464374B1/en not_active Expired - Lifetime
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